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CN108087871A - A kind of coal burner - Google Patents

A kind of coal burner Download PDF

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Publication number
CN108087871A
CN108087871A CN201810076910.6A CN201810076910A CN108087871A CN 108087871 A CN108087871 A CN 108087871A CN 201810076910 A CN201810076910 A CN 201810076910A CN 108087871 A CN108087871 A CN 108087871A
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China
Prior art keywords
combustion chamber
primary
air
air duct
primary air
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Pending
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CN201810076910.6A
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Chinese (zh)
Inventor
徐夕仁
文继成
崔琳
张凯
董磊
马文明
陈余祥
陈莲芳
张赞
朱玉花
杨桂琥
姜静
乔振云
徐仰连
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Shandong Energy Cleaning Group Yu Jie Environmental Protection Engineering Co Ltd
Shandong University
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Shandong Energy Cleaning Group Yu Jie Environmental Protection Engineering Co Ltd
Shandong University
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Application filed by Shandong Energy Cleaning Group Yu Jie Environmental Protection Engineering Co Ltd, Shandong University filed Critical Shandong Energy Cleaning Group Yu Jie Environmental Protection Engineering Co Ltd
Priority to CN201810076910.6A priority Critical patent/CN108087871A/en
Publication of CN108087871A publication Critical patent/CN108087871A/en
Pending legal-status Critical Current

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Classifications

    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F23COMBUSTION APPARATUS; COMBUSTION PROCESSES
    • F23DBURNERS
    • F23D1/00Burners for combustion of pulverulent fuel
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F23COMBUSTION APPARATUS; COMBUSTION PROCESSES
    • F23CMETHODS OR APPARATUS FOR COMBUSTION USING FLUID FUEL OR SOLID FUEL SUSPENDED IN  A CARRIER GAS OR AIR 
    • F23C6/00Combustion apparatus characterised by the combination of two or more combustion chambers or combustion zones, e.g. for staged combustion
    • F23C6/04Combustion apparatus characterised by the combination of two or more combustion chambers or combustion zones, e.g. for staged combustion in series connection
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F23COMBUSTION APPARATUS; COMBUSTION PROCESSES
    • F23CMETHODS OR APPARATUS FOR COMBUSTION USING FLUID FUEL OR SOLID FUEL SUSPENDED IN  A CARRIER GAS OR AIR 
    • F23C7/00Combustion apparatus characterised by arrangements for air supply
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F23COMBUSTION APPARATUS; COMBUSTION PROCESSES
    • F23LSUPPLYING AIR OR NON-COMBUSTIBLE LIQUIDS OR GASES TO COMBUSTION APPARATUS IN GENERAL ; VALVES OR DAMPERS SPECIALLY ADAPTED FOR CONTROLLING AIR SUPPLY OR DRAUGHT IN COMBUSTION APPARATUS; INDUCING DRAUGHT IN COMBUSTION APPARATUS; TOPS FOR CHIMNEYS OR VENTILATING SHAFTS; TERMINALS FOR FLUES
    • F23L1/00Passages or apertures for delivering primary air for combustion 
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F23COMBUSTION APPARATUS; COMBUSTION PROCESSES
    • F23LSUPPLYING AIR OR NON-COMBUSTIBLE LIQUIDS OR GASES TO COMBUSTION APPARATUS IN GENERAL ; VALVES OR DAMPERS SPECIALLY ADAPTED FOR CONTROLLING AIR SUPPLY OR DRAUGHT IN COMBUSTION APPARATUS; INDUCING DRAUGHT IN COMBUSTION APPARATUS; TOPS FOR CHIMNEYS OR VENTILATING SHAFTS; TERMINALS FOR FLUES
    • F23L9/00Passages or apertures for delivering secondary air for completing combustion of fuel 

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  • Engineering & Computer Science (AREA)
  • Chemical & Material Sciences (AREA)
  • Combustion & Propulsion (AREA)
  • Mechanical Engineering (AREA)
  • General Engineering & Computer Science (AREA)

Abstract

本发明涉及一种煤粉燃烧器,属于煤粉燃烧设备技术领域,其内部设有预燃室,还包括微波等离子点火组件、一次风组件和二次风组件,所述预燃室的内部设有相连通且平行的一级预燃室和二级预燃室,所述一次风组件包括一次风母管、煤粉浓缩器和风道隔板,本发明借助微波等离子点火组件产生高温等离子体,做为高温点火或助燃热源,强化了低负荷时燃烧的稳定性,特别适合于锅炉频繁启停负荷变化大的情况,对一次风进行浓淡分离,有助于燃烧稳定,降低了氮氧化物的生成量,提高了燃烧效率,同时,借助浓一次风环形通道和二次风通道,避免预燃室产生结焦现象,从而实现全负荷高效、低污染燃烧。

The invention relates to a pulverized coal burner, which belongs to the technical field of pulverized coal combustion equipment. It is equipped with a pre-combustion chamber inside, and also includes a microwave plasma ignition assembly, a primary air assembly and a secondary air assembly. There are connected and parallel primary pre-combustion chambers and secondary pre-combustion chambers. The primary air assembly includes a primary air main pipe, a pulverized coal concentrator and an air duct partition. The present invention generates high-temperature plasma by means of a microwave plasma ignition assembly. As a high-temperature ignition or combustion-supporting heat source, it enhances the stability of combustion at low loads, and is especially suitable for situations where the boiler frequently starts and stops and the load changes greatly. Separating the primary air from thick and thin helps to stabilize combustion and reduce the emission of nitrogen oxides. At the same time, with the help of the dense primary air annular channel and the secondary air channel, the coking phenomenon in the pre-combustion chamber is avoided, so as to achieve high-efficiency and low-pollution combustion at full load.

Description

一种煤粉燃烧器a pulverized coal burner

技术领域technical field

本发明属于煤粉燃烧设备技术领域,具体地说涉及一种煤粉燃烧器。The invention belongs to the technical field of pulverized coal combustion equipment, and in particular relates to a pulverized coal burner.

背景技术Background technique

相对于大容量的电站锅炉,燃煤工业锅炉具有燃煤流量小、炉膛容积小的特点,导致其燃烧器的稳燃情况、炉内热量流动及燃烧情况都较难控制,制约着燃煤工业锅炉全面推广应用。Compared with large-capacity power plant boilers, coal-fired industrial boilers have the characteristics of small coal-fired flow and small furnace volume, which makes it difficult to control the stable combustion of the burner, heat flow and combustion in the furnace, and restricts the coal-fired industry. Comprehensive promotion and application of boilers.

近几年,市场上出现了几种燃煤工业锅炉用的燃烧器。其中,北京煤炭科学技术研究院有限公司借鉴Dr.schoppe燃烧器的燃烧组织原理设计了中心逆喷双锥燃烧器,相较于其他旋流式燃烧器,该燃烧器单独设立双锥形回流室(预燃室),靠旋转的二次风流场形成回流区,靠一次风(煤粉空气混合物)中心逆喷强化高温烟气回流,有利地强化了煤粉气流在回流室内的气化着火和燃烧,有利于着火和燃烧,同时,也存在回流室壁面(特别是出口附近)结焦、喷粉管过热变形、氮氧化物排放浓度高等问题。上海市特种设备监督检验技术研究院设计出低流量煤粉稳燃燃烧器,利用内二次风旋流器的作用和一次风粉混合物通道出口设置的钝体,形成一个稳定的回流区,在回流区内充满由炉膛中心回流来的高温烟气,在回流区外侧与主流区之间的区域,形成可燃烧气粉混合物和热回流烟气湍流混合区。由于在边界上有较大的径向速度梯度,可燃混合物和高温烟气之间发生强烈的质量、动量和能量交换,可燃混合物不断被加热升温,达到着火温度开始着火,同时,火焰由内向外传播,将热量传给回流的烟气,使烟气将热能带往上游,再把热量传给新的可燃混合物,在预燃室内形成稳定燃烧。虽然该设计充满度较好,也形成了易于煤粉气流着火燃烧的流场和温度环境,但是,高温烟气过早与二次风混合,火焰过于靠近预燃室壁面,存在壁面结渣烧坏的问题。In recent years, several types of burners for coal-fired industrial boilers have appeared on the market. Among them, Beijing Coal Science and Technology Research Institute Co., Ltd. designed a center reverse injection double cone burner by referring to the combustion organization principle of Dr.schoppe burner. Compared with other swirl burners, this burner has a separate double cone recirculation chamber (Pre-combustion chamber), the recirculation zone is formed by the rotating secondary air flow field, and the high-temperature flue gas reflow is strengthened by the reverse injection of the primary air (powdered coal-air mixture) center, which advantageously strengthens the gasification and ignition of the pulverized coal airflow in the recirculation chamber. Combustion is conducive to ignition and combustion. At the same time, there are also problems such as coking on the wall of the reflow chamber (especially near the outlet), overheating and deformation of the powder injection tube, and high concentration of nitrogen oxide emissions. The Shanghai Special Equipment Supervision and Inspection Technology Research Institute has designed a low-flow pulverized coal stable combustion burner, which uses the function of the internal secondary air cyclone and the blunt body set at the outlet of the primary air-powder mixture channel to form a stable recirculation zone. The recirculation zone is filled with high-temperature flue gas reflowed from the center of the furnace, and a turbulent mixing zone of combustible gas powder mixture and hot recirculation flue gas is formed in the area between the outside of the recirculation zone and the main flow zone. Due to the large radial velocity gradient at the boundary, there is a strong exchange of mass, momentum and energy between the combustible mixture and the high-temperature flue gas, and the combustible mixture is continuously heated up until it reaches the ignition temperature and starts to ignite. At the same time, the flame flows from the inside to the outside Propagation, the heat is transferred to the returning flue gas, so that the flue gas will bring the heat energy to the upstream, and then transfer the heat to the new combustible mixture to form a stable combustion in the pre-combustion chamber. Although the fullness of this design is good, it also forms a flow field and temperature environment that is easy for the pulverized coal to ignite and burn. However, the high-temperature flue gas mixes with the secondary air too early, and the flame is too close to the wall of the pre-combustion chamber, causing slagging on the wall. bad question.

同时,在电站锅炉燃烧器领域,为了降低点火用油的成本,各有关单位相继开发了新的煤粉锅炉点火技术,如等离子体点火技术、微油点火技术、富氧点火技术等。常规的等离子点火技术是利用直流电流(280-350A)在介质气压0.01-0.03MPa的条件下接触引弧,并在强磁场下获得稳定功率的直流空气等离子体。与传统的燃油相比具有经济、环保、高效、简单安全的特点,是目前燃油系统改造的替代产品。然而,运用等离子体电弧点燃煤粉的燃烧器一般采用等离子体发生器轴向插入方式,一次风管内设置多级导筒,煤粉被逐级分配,进入一级导筒内的煤粉被等离子火焰点燃后,再点燃进入二级导筒内的煤粉,并以此类推,剩余的导筒内的煤粉依次被点燃。一般导筒共分三级在每级导筒及一次风管内设置浓淡导流环,使得浓相煤粉进入中心区域,便于煤粉的点燃。这种燃烧器一般都对原有燃烧器的改动较大,使燃烧器内部的流场、温度分布、喷口处的燃烧区域均发生变化,浓相的煤粉沿燃烧器的中心线分布,不仅影响燃烧器的性能,促使燃烧器无法恢复原有的煤粉浓淡分离状态,而且破坏了燃烧器喷口处进入炉膛处的温度分布。At the same time, in the field of power plant boiler burners, in order to reduce the cost of ignition oil, various relevant units have successively developed new ignition technologies for pulverized coal boilers, such as plasma ignition technology, micro-oil ignition technology, and oxygen-enriched ignition technology. Conventional plasma ignition technology uses direct current (280-350A) to contact arc ignition under the condition of medium pressure 0.01-0.03MPa, and obtains stable power DC air plasma under strong magnetic field. Compared with traditional fuel oil, it has the characteristics of economy, environmental protection, high efficiency, simplicity and safety, and is a substitute product for the transformation of the current fuel system. However, the burner that uses the plasma arc to ignite pulverized coal generally adopts the axial insertion method of the plasma generator. The primary air duct is equipped with multi-stage guide tubes, and the pulverized coal is distributed step by step. After the flame is ignited, the pulverized coal entering the secondary guide tube is ignited again, and by analogy, the pulverized coal in the remaining guide tube is ignited in turn. Generally, the guide tube is divided into three levels, and a thick-thin guide ring is set in each level of the guide tube and the primary air duct, so that the dense-phase coal powder enters the central area, which is convenient for the ignition of the coal powder. This kind of burner generally changes the original burner greatly, so that the flow field, temperature distribution inside the burner, and the combustion area at the nozzle all change, and the dense phase coal powder is distributed along the center line of the burner, not only It affects the performance of the burner, making the burner unable to restore the original state of separation of pulverized coal concentration and light, and destroying the temperature distribution at the burner nozzle entering the furnace.

发明内容Contents of the invention

针对现有技术的种种不足,为了解决上述问题,现提出一种煤粉燃烧器。Aiming at the various deficiencies of the prior art, in order to solve the above problems, a pulverized coal burner is now proposed.

为实现上述目的,本发明提供如下技术方案:To achieve the above object, the present invention provides the following technical solutions:

一种煤粉燃烧器,其内部设有预燃室,还包括微波等离子点火组件、一次风组件和二次风组件,所述预燃室的内部设有相连通且平行的一级预燃室和二级预燃室,所述一级预燃室位于二级预燃室的进口端,所述二级预燃室的出口端与锅炉炉膛连通,所述微波等离子点火组件、一次风组件位于一级预燃室的进口端,且微波等离子点火组件与一级预燃室的中心轴线重合,所述二次风组件套设在预燃室的外围;A pulverized coal burner, which is provided with a pre-combustion chamber inside, and also includes a microwave plasma ignition assembly, a primary air assembly and a secondary air assembly, and the inside of the pre-combustion chamber is provided with a connected and parallel primary and a secondary pre-combustion chamber, the primary pre-combustion chamber is located at the inlet end of the secondary pre-combustion chamber, the outlet end of the secondary pre-combustion chamber communicates with the boiler furnace, the microwave plasma ignition assembly and the primary air assembly are located at The inlet end of the primary pre-chamber, and the microwave plasma ignition assembly coincides with the central axis of the primary pre-chamber, and the secondary air assembly is sleeved on the periphery of the pre-chamber;

所述一次风组件包括一次风母管、煤粉浓缩器和风道隔板,所述一次风母管包括相垂直且连通的垂直风管和水平风管,所述煤粉浓缩器和风道隔板位于垂直风管内部,所述一级预燃室位于水平风管内部,所述风道隔板沿着垂直方向设置并与一级预燃室的外壁相接,且其将垂直风管分隔为浓一次风道和淡一次风道,所述浓一次风道与一级预燃室的进口端连通,所述淡一次风道与二级预燃室的进口端连通,所述浓一次风道的管径小于淡一次风道的管径。The primary air assembly includes a primary air main pipe, a pulverized coal concentrator and an air duct partition. The primary air main pipe includes vertical and connected vertical air ducts and horizontal air ducts. Located inside the vertical air duct, the primary pre-combustion chamber is located inside the horizontal air duct, the air duct partition is arranged along the vertical direction and connected with the outer wall of the primary pre-combustion chamber, and it divides the vertical air duct into A thick primary air duct and a light primary air duct, the thick primary air duct communicates with the inlet end of the primary pre-combustion chamber, the light primary air duct communicates with the inlet end of the secondary pre-combustion chamber, and the rich primary air duct The diameter of the pipe is smaller than that of the primary air duct.

进一步,所述一级预燃室和二级预燃室均设为圆筒结构,且两者的外壁材料均为不锈钢板。Further, the primary pre-chamber and the secondary pre-chamber are both cylindrical structures, and the outer wall materials of both are stainless steel plates.

进一步,所述二级预燃室的进口端正对水平风管设置,且两者的直径相同,所述一级预燃室的外壁与水平风管的外壁之间留有与淡一次风道连通的淡一次风环形通道。Further, the inlet end of the secondary pre-combustion chamber is set facing the horizontal air duct, and the diameters of both are the same, and there is a gap between the outer wall of the primary pre-combustion chamber and the outer wall of the horizontal air duct to communicate with the primary air duct. The light primary wind circular channel.

进一步,所述风道隔板与一级预燃室的外壁相接处设有倾斜隔板,所述垂直风管和水平风管相接处设有锥形体,所述锥形体的锥面与倾斜隔板平行,且两者之间留有与浓一次风道连通的浓一次风环形通道。Further, an inclined partition is provided at the joint between the air channel partition and the outer wall of the primary pre-combustion chamber, and a cone is provided at the joint between the vertical air duct and the horizontal air duct, and the conical surface of the cone is in contact with the outer wall of the primary pre-combustion chamber. The inclined partitions are parallel, and there is an annular passage for the concentrated primary air communicated with the concentrated primary air passage between them.

进一步,所述淡一次风环形通道与二级预燃室的进口端连通,所述浓一次风环形通道与一级预燃室的进口端连通。Further, the annular channel of the weak primary air communicates with the inlet end of the secondary pre-combustion chamber, and the annular channel of the rich primary air communicates with the inlet end of the primary pre-combustion chamber.

进一步,所述倾斜隔板与水平面的夹角为30°-40°。Further, the angle between the inclined partition and the horizontal plane is 30°-40°.

进一步,所述二次风组件包括二次风进口、风箱和旋流器,所述风箱套设在预燃室的外围,所述二次风进口、旋流器分别位于风箱的两端,且旋流器位于预燃室的进口端。Further, the secondary air assembly includes a secondary air inlet, an air box and a swirler, the air box is sleeved on the periphery of the pre-combustion chamber, the secondary air inlet and the swirler are respectively located at both ends of the air box, and The swirler is located at the inlet end of the pre-chamber.

进一步,所述二级预燃室的外壁与预燃室的外壁之间留有与旋流器连通的二次风通道,所述二次风通道的出口端与锅炉炉膛连通。Further, there is a secondary air channel communicating with the swirler between the outer wall of the secondary pre-combustion chamber and the outer wall of the pre-combustion chamber, and the outlet end of the secondary air channel communicates with the boiler furnace.

进一步,所述微波等离子点火组件包括微波等离子体发生器和微波发生器,所述微波等离子体发生器的等离子喷口与一级预燃室的进口端连通,且两者正对设置,所述微波发生器通过微波耦合管与微波等离子体发生器连接。Further, the microwave plasma ignition assembly includes a microwave plasma generator and a microwave generator, the plasma nozzle of the microwave plasma generator communicates with the inlet end of the first-stage pre-combustion chamber, and the two are facing each other, and the microwave The generator is connected with the microwave plasma generator through a microwave coupling tube.

本发明的有益效果是:The beneficial effects of the present invention are:

借助微波等离子点火组件产生高温等离子体,做为高温点火或助燃热源,强化了低负荷时燃烧的稳定性,特别适合于锅炉频繁启停负荷变化大的情况,对一次风进行浓淡分离,有助于燃烧稳定,降低了氮氧化物的生成量,提高了燃烧效率,同时,借助浓一次风环形通道和二次风通道,避免预燃室产生结焦现象,从而实现全负荷高效、低污染燃烧。High-temperature plasma is generated by means of microwave plasma ignition components as a high-temperature ignition or combustion-supporting heat source, which enhances the stability of combustion at low loads, and is especially suitable for situations where the boiler frequently starts and stops and the load changes greatly. Separating the concentration of primary air is helpful Because of the stable combustion, the generation of nitrogen oxides is reduced, and the combustion efficiency is improved. At the same time, with the help of the dense primary air annular channel and the secondary air channel, the coking phenomenon in the pre-combustion chamber is avoided, so as to achieve full-load high-efficiency and low-pollution combustion.

附图说明Description of drawings

图1是本发明的整体结构示意图;Fig. 1 is the overall structural representation of the present invention;

图2是一次风组件结构示意图。Fig. 2 is a schematic structural diagram of the primary air component.

附图中:1-预燃室、2-一级预燃室、3-二级预燃室、4-一次风母管、401-垂直风管、402-水平风管、5-一次风、6-二次风、7-二次风进口、8-风箱、9-旋流器、10-微波等离子体发生器、11-微波发生器、12-煤粉浓缩器、13-风道隔板、14-浓一次风道、15-淡一次风道、16-倾斜隔板、17-浓一次风环形通道、18-淡一次风环形通道、19-二次风通道、20-锥形体。In the drawings: 1- pre-combustion chamber, 2- primary pre-combustion chamber, 3- secondary pre-combustion chamber, 4- primary air duct, 401- vertical air duct, 402- horizontal air duct, 5- primary air, 6-secondary air, 7-secondary air inlet, 8-air box, 9-cyclone, 10-microwave plasma generator, 11-microwave generator, 12-coal powder concentrator, 13-air duct partition , 14-concentrated primary air duct, 15-light primary air duct, 16-inclined partition, 17-concentrated primary air annular channel, 18-light primary air annular channel, 19-secondary air channel, 20-conical body.

具体实施方式Detailed ways

为了使本领域的人员更好地理解本发明的技术方案,下面结合本发明的附图,对本发明的技术方案进行清楚、完整的描述,基于本申请中的实施例,本领域普通技术人员在没有做出创造性劳动的前提下所获得的其它类同实施例,都应当属于本申请保护的范围。此外,以下实施例中提到的方向用词,例如“上”“下”“左”“右”等仅是参考附图的方向,因此,使用的方向用词是用来说明而非限制本发明创造。In order to make those skilled in the art better understand the technical solution of the present invention, the technical solution of the present invention is clearly and completely described below in conjunction with the accompanying drawings of the present invention. Based on the embodiments in this application, those of ordinary skill in the art will Other similar embodiments obtained without creative work shall all fall within the scope of protection of this application. In addition, the directional words mentioned in the following embodiments, such as "upper", "lower", "left", "right", etc., are only referring to the directions of the drawings, therefore, the directional words used are for illustration rather than limitation invent.

实施例一:Embodiment one:

如图1-2所示,一种煤粉燃烧器,其内部设有预燃室1,还包括微波等离子点火组件、一次风组件和二次风组件。其中,所述预燃室1的内部设有相连通且平行的一级预燃室2和二级预燃室3,所述一级预燃室2位于二级预燃室3的进口端,而二级预燃室3的出口端与锅炉炉膛连通。As shown in Figure 1-2, a pulverized coal burner has a pre-combustion chamber 1 inside, and also includes a microwave plasma ignition assembly, a primary air assembly and a secondary air assembly. Wherein, the inside of the pre-chamber 1 is provided with a connected and parallel primary pre-chamber 2 and a secondary pre-chamber 3, the primary pre-chamber 2 is located at the inlet end of the secondary pre-chamber 3, And the outlet end of the secondary pre-combustion chamber 3 communicates with the boiler furnace.

所述微波等离子点火组件位于一级预燃室2的进口端,且微波等离子点火组件与一级预燃室2的中心轴线重合,所述微波等离子点火组件包括微波等离子体发生器10和微波发生器11,所述微波等离子体发生器10的等离子喷口与一级预燃室2的进口端连通,且两者正对设置,所述微波发生器11通过微波耦合管与微波等离子体发生器10连接。也就是说,微波等离子体发生器10把微波发生器11产生的微波转变成等离子体,起到煤粉点火和助燃的作用。同时,微波等离子体发生器10、一级预燃室2、二级预燃室3串联连接,起到热量放大作用,利用少量电能点燃较多的煤粉,使煤粉进入锅炉炉膛前已基本气化,有利于未燃尽煤粉和气体可燃物在锅炉炉膛的继续燃烧和燃尽。The microwave plasma ignition assembly is located at the inlet end of the primary pre-chamber 2, and the microwave plasma ignition assembly coincides with the central axis of the primary pre-chamber 2, and the microwave plasma ignition assembly includes a microwave plasma generator 10 and a microwave generator device 11, the plasma nozzle of the microwave plasma generator 10 communicates with the inlet end of the primary pre-combustion chamber 2, and the two are facing to each other, and the microwave generator 11 is connected to the microwave plasma generator 10 through a microwave coupling tube connect. That is to say, the microwave plasma generator 10 converts the microwave generated by the microwave generator 11 into plasma, which plays the role of coal powder ignition and combustion support. At the same time, the microwave plasma generator 10, the primary pre-combustion chamber 2, and the secondary pre-combustion chamber 3 are connected in series to amplify the heat, and use a small amount of electric energy to ignite more pulverized coal, so that the pulverized coal is basically Gasification is beneficial to the continuous combustion and burnout of unburned pulverized coal and gaseous combustibles in the boiler furnace.

所述一次风组件位于一级预燃室2的进口端,其包括一次风母管4、煤粉浓缩器12和风道隔板13。所述一次风母管4包括相垂直且连通的垂直风管401和水平风管402,所述煤粉浓缩器12和风道隔板13位于垂直风管401内部,所述一级预燃室2位于水平风管402内部。煤粉浓缩器12将一次风5(煤粉空气混合物)分离成浓、淡两股,即浓一次风和淡一次风,同时,所述风道隔板13沿着垂直方向设置并与一级预燃室2的外壁相接,且其将垂直风管401分隔为浓一次风道14和淡一次风道15,分别用于导流浓一次风和淡一次风。所述浓一次风道14与一级预燃室2的进口端连通,所述淡一次风道15与二级预燃室3的进口端连通,且浓一次风道14的管径小于淡一次风道15的管径,也就是说,少量浓一次风进入一级预燃室2,可以利用较小能量的等离子体火焰(约4000℃)快速加热分解浓一次风中的煤粉,形成高温燃气(温度为1100-1200℃),随后高温燃气进入二级预燃室3,与淡一次风相遇,在高温燃气加热及燃烧放热的作用下,淡一次风中的煤粉被燃烧气化。The primary air assembly is located at the inlet end of the primary pre-combustion chamber 2 , and includes a primary air main pipe 4 , a pulverized coal concentrator 12 and an air duct partition 13 . The primary air duct 4 includes a vertical and connected vertical air duct 401 and a horizontal air duct 402, the pulverized coal concentrator 12 and the air duct partition 13 are located inside the vertical air duct 401, and the primary pre-combustion chamber 2 Located inside the horizontal air duct 402. The pulverized coal concentrator 12 separates the primary air 5 (powdered coal air mixture) into thick and light two strands, i.e. thick primary air and light primary air. The outer walls of the pre-combustion chamber 2 are connected, and it divides the vertical air duct 401 into a rich primary air channel 14 and a weak primary air channel 15, which are used to divert the rich primary air and the light primary air respectively. The thick primary air channel 14 communicates with the inlet end of the primary pre-combustion chamber 2, and the light primary air channel 15 communicates with the inlet end of the secondary pre-combustion chamber 3, and the diameter of the rich primary air channel 14 is smaller than that of the light primary air channel. The pipe diameter of the air duct 15, that is to say, a small amount of concentrated primary air enters the first-stage pre-combustion chamber 2, and a plasma flame (about 4000° C.) with less energy can be used to rapidly heat and decompose the coal powder in the concentrated primary air to form a high temperature Gas (temperature is 1100-1200°C), then the high-temperature gas enters the secondary pre-combustion chamber 3, meets the light primary air, and under the action of high-temperature gas heating and combustion heat release, the coal powder in the light primary air is burned and gasified .

所述一级预燃室2和二级预燃室3均设为圆筒结构,且两者的外壁材料均为不锈钢板,内衬耐热材料。所述二级预燃室3的进口端正对水平风管402设置,且两者的直径相同,所述一级预燃室2的外壁与水平风管402的外壁之间留有与淡一次风道15连通的淡一次风环形通道18,且淡一次风环形通道18与二级预燃室3的进口端连通,也就是说,淡一次风呈环形进入二级预燃室3,避免产生结焦现象。同时,所述风道隔板13与一级预燃室2的外壁相接处设有倾斜隔板16,本实施例中,所述风道隔板13与倾斜隔板16一体成型。所述垂直风管401和水平风管402相接处设有锥形体20,所述锥形体20的锥面与倾斜隔板16平行,且两者之间留有与浓一次风道14连通的浓一次风环形通道17,且浓一次风环形通道17与一级预燃室2的进口端连通,也就是说,浓一次风呈环形进入一级预燃室2,等离子体火焰被浓一次风环绕,为强化浓一次风与等离子体火焰的混合加热,所述倾斜隔板16与水平面的夹角为30°-40°,使浓一次风按一定角度喷入等离子体火焰中。Both the primary pre-combustion chamber 2 and the secondary pre-combustion chamber 3 are in a cylindrical structure, and the outer walls of both are made of stainless steel plates and lined with heat-resistant materials. The inlet end of the secondary pre-combustion chamber 3 is arranged facing the horizontal air duct 402, and the diameters of the two are the same, and there is a weak primary air between the outer wall of the primary pre-combustion chamber 2 and the outer wall of the horizontal air duct 402. The light primary air annular channel 18 communicated with the road 15, and the light primary air annular channel 18 communicates with the inlet end of the secondary pre-combustion chamber 3, that is to say, the light primary air enters the secondary pre-combustion chamber 3 in a ring shape to avoid coking Phenomenon. At the same time, an inclined partition 16 is provided at the junction between the air duct partition 13 and the outer wall of the primary pre-combustion chamber 2 , and in this embodiment, the air duct partition 13 and the inclined partition 16 are integrally formed. The junction of the vertical air duct 401 and the horizontal air duct 402 is provided with a conical body 20, the conical surface of the conical body 20 is parallel to the inclined partition 16, and there is a gap between the two that communicates with the primary air duct 14. The thick primary air annular passage 17, and the thick primary air annular passage 17 is connected with the inlet end of the first-level pre-combustion chamber 2, that is to say, the thick primary air enters the first-level pre-combustion chamber 2 in a ring shape, and the plasma flame is blown by the thick primary air. Surrounding, in order to strengthen the mixed heating of the concentrated primary air and the plasma flame, the angle between the inclined partition 16 and the horizontal plane is 30°-40°, so that the concentrated primary air is sprayed into the plasma flame at a certain angle.

所述二次风组件套设在预燃室1的外围,其包括二次风进口7、风箱8和旋流器9,所述风箱8套设在预燃室1的外围,所述二次风进口7、旋流器9分别位于风箱8的两端,且旋流器9位于预燃室1的进口端,也就是说,二次风6进入后,向燃烧器的进口端反向流动。所述二级预燃室3的外壁与预燃室1的外壁之间留有与旋流器9连通的二次风通道19,所述二次风通道19的出口端与锅炉炉膛连通,即离开二级预燃室3的高温燃气(温度为800-900℃)在锅炉炉膛内与二次风相遇,形成旋流燃烧流场,有助于燃烧稳定和燃尽,同时,一级预燃室2和二级预燃室3内部是强还原性气氛,有利于抑制氮氧化物的产生。The secondary air assembly is sleeved on the periphery of the pre-combustion chamber 1, and includes a secondary air inlet 7, an air box 8 and a swirler 9, the wind box 8 is sleeved on the periphery of the pre-chamber 1, and the secondary air The air inlet 7 and the swirler 9 are respectively located at both ends of the wind box 8, and the swirler 9 is located at the inlet end of the pre-combustion chamber 1, that is to say, after the secondary air 6 enters, it flows in the opposite direction to the inlet end of the burner . A secondary air channel 19 communicated with the swirler 9 is left between the outer wall of the secondary pre-combustion chamber 3 and the outer wall of the pre-combustion chamber 1, and the outlet end of the secondary air channel 19 communicates with the boiler furnace, that is, The high-temperature gas (temperature 800-900°C) leaving the secondary pre-combustion chamber 3 meets the secondary air in the boiler furnace to form a swirling combustion flow field, which is conducive to stable combustion and burnout. At the same time, the primary pre-combustion The interior of the chamber 2 and the secondary pre-combustion chamber 3 is a strong reducing atmosphere, which is beneficial to suppress the generation of nitrogen oxides.

以上已将本发明做一详细说明,以上所述,仅为本发明之较佳实施例而已,当不能限定本发明实施范围,即凡依本申请范围所作均等变化与修饰,皆应仍属本发明涵盖范围内。The present invention has been described in detail above. The foregoing description is only a preferred embodiment of the present invention, and should not limit the implementation scope of the present invention. within the scope of the invention.

Claims (9)

1.一种煤粉燃烧器,其内部设有预燃室,其特征在于,还包括微波等离子点火组件、一次风组件和二次风组件,所述预燃室的内部设有相连通且平行的一级预燃室和二级预燃室,所述一级预燃室位于二级预燃室的进口端,所述二级预燃室的出口端与锅炉炉膛连通,所述微波等离子点火组件、一次风组件位于一级预燃室的进口端,且微波等离子点火组件与一级预燃室的中心轴线重合,所述二次风组件套设在预燃室的外围;1. A pulverized coal burner, which is provided with a pre-combustion chamber inside, is characterized in that it also includes a microwave plasma ignition assembly, a primary air assembly and a secondary air assembly, and the inside of the pre-combustion chamber is provided with connected and parallel The primary pre-combustion chamber and the secondary pre-combustion chamber, the primary pre-combustion chamber is located at the inlet end of the secondary pre-combustion chamber, the outlet end of the secondary pre-combustion chamber communicates with the boiler furnace, and the microwave plasma ignition The component and the primary air component are located at the inlet end of the primary pre-combustion chamber, and the microwave plasma ignition component coincides with the central axis of the primary pre-combustion chamber, and the secondary air component is sleeved on the periphery of the pre-combustion chamber; 所述一次风组件包括一次风母管、煤粉浓缩器和风道隔板,所述一次风母管包括相垂直且连通的垂直风管和水平风管,所述煤粉浓缩器和风道隔板位于垂直风管内部,所述一级预燃室位于水平风管内部,所述风道隔板沿着垂直方向设置并与一级预燃室的外壁相接,且其将垂直风管分隔为浓一次风道和淡一次风道,所述浓一次风道与一级预燃室的进口端连通,所述淡一次风道与二级预燃室的进口端连通,所述浓一次风道的管径小于淡一次风道的管径。The primary air assembly includes a primary air main pipe, a pulverized coal concentrator and an air duct partition. The primary air main pipe includes vertical and connected vertical air ducts and horizontal air ducts. Located inside the vertical air duct, the primary pre-combustion chamber is located inside the horizontal air duct, the air duct partition is arranged along the vertical direction and connected with the outer wall of the primary pre-combustion chamber, and it divides the vertical air duct into A thick primary air duct and a light primary air duct, the thick primary air duct communicates with the inlet end of the primary pre-combustion chamber, the light primary air duct communicates with the inlet end of the secondary pre-combustion chamber, and the rich primary air duct The diameter of the pipe is smaller than that of the primary air duct. 2.根据权利要求1所述的一种煤粉燃烧器,其特征在于,所述一级预燃室和二级预燃室均设为圆筒结构,且两者的外壁材料均为不锈钢板。2. A pulverized coal burner according to claim 1, characterized in that, the primary pre-combustion chamber and the secondary pre-combustion chamber are both cylindrical structures, and the outer wall materials of both are stainless steel plates . 3.根据权利要求2所述的一种煤粉燃烧器,其特征在于,所述二级预燃室的进口端正对水平风管设置,且两者的直径相同,所述一级预燃室的外壁与水平风管的外壁之间留有与淡一次风道连通的淡一次风环形通道。3. A pulverized coal burner according to claim 2, characterized in that, the inlet end of the secondary pre-combustion chamber is arranged facing the horizontal air duct, and both have the same diameter, and the primary pre-combustion chamber A light primary air annular passage communicated with the light primary air duct is left between the outer wall of the horizontal air duct and the outer wall of the horizontal air duct. 4.根据权利要求3所述的一种煤粉燃烧器,其特征在于,所述风道隔板与一级预燃室的外壁相接处设有倾斜隔板,所述垂直风管和水平风管相接处设有锥形体,所述锥形体的锥面与倾斜隔板平行,且两者之间留有与浓一次风道连通的浓一次风环形通道。4. A pulverized coal burner according to claim 3, characterized in that an inclined partition is provided at the joint between the air passage partition and the outer wall of the primary pre-combustion chamber, and the vertical air duct and the horizontal A conical body is provided at the junction of the air ducts, the conical surface of the conical body is parallel to the inclined partition, and there is an annular passage for the concentrated primary air communicating with the concentrated primary air passage between the two. 5.根据权利要求4所述的一种煤粉燃烧器,其特征在于,所述淡一次风环形通道与二级预燃室的进口端连通,所述浓一次风环形通道与一级预燃室的进口端连通。5. A pulverized coal burner according to claim 4, characterized in that, said light primary air annular channel communicates with the inlet end of the secondary pre-combustion chamber, said thick primary air annular channel communicates with the primary pre-combustion chamber The inlet end of the chamber is connected. 6.根据权利要求4所述的一种煤粉燃烧器,其特征在于,所述倾斜隔板与水平面的夹角为30°-40°。6. A pulverized coal burner according to claim 4, characterized in that the angle between the inclined partition and the horizontal plane is 30°-40°. 7.根据权利要求2-6任一所述的一种煤粉燃烧器,其特征在于,所述二次风组件包括二次风进口、风箱和旋流器,所述风箱套设在预燃室的外围,所述二次风进口、旋流器分别位于风箱的两端,且旋流器位于预燃室的进口端。7. A pulverized coal burner according to any one of claims 2-6, characterized in that, the secondary air assembly includes a secondary air inlet, an air box and a swirler, and the air box is sleeved on the pre-combustion The periphery of the chamber, the secondary air inlet and the swirler are respectively located at both ends of the air box, and the swirler is located at the inlet end of the pre-combustion chamber. 8.根据权利要求7所述的一种煤粉燃烧器,其特征在于,所述二级预燃室的外壁与预燃室的外壁之间留有与旋流器连通的二次风通道,所述二次风通道的出口端与锅炉炉膛连通。8. A kind of pulverized coal burner according to claim 7, it is characterized in that, there is a secondary air passage communicated with the swirler between the outer wall of the secondary pre-combustion chamber and the outer wall of the pre-combustion chamber, The outlet end of the secondary air channel communicates with the furnace of the boiler. 9.根据权利要求7所述的一种煤粉燃烧器,其特征在于,所述微波等离子点火组件包括微波等离子体发生器和微波发生器,所述微波等离子体发生器的等离子喷口与一级预燃室的进口端连通,且两者正对设置,所述微波发生器通过微波耦合管与微波等离子体发生器连接。9. A kind of pulverized coal burner according to claim 7, it is characterized in that, described microwave plasma ignition assembly comprises microwave plasma generator and microwave generator, and the plasma spout of described microwave plasma generator is connected with primary The inlet end of the pre-combustion chamber is communicated, and the two are arranged facing each other, and the microwave generator is connected with the microwave plasma generator through a microwave coupling tube.
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Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN109140433A (en) * 2018-08-21 2019-01-04 煤科院节能技术有限公司 A kind of bipyramid preventing primary air piping overheating deforming is against coal powder injection powder burner
CN113028390A (en) * 2021-04-19 2021-06-25 煤科院节能技术有限公司 Small-capacity biomass powder fuel boiler
CN115247785A (en) * 2020-11-12 2022-10-28 王永 A plasma cracking combustion device

Citations (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2002228107A (en) * 2001-01-31 2002-08-14 Mitsubishi Heavy Ind Ltd Pulverized coal burner
CN101021319A (en) * 2007-02-26 2007-08-22 杭州意能节能技术有限公司 Concentrated and thin fuel-saving igniting coal powder burner
CN101403497A (en) * 2008-11-12 2009-04-08 哈尔滨工业大学 Micro-oil ignition rotational flow breeze combustion device for preventing slag bonding of primary combustion chamber
CN201615480U (en) * 2010-02-09 2010-10-27 济南海普电力节能科技有限公司 Pulverized coal boiler microwave plasma preheating pulverized coal gasification small oil gun ignition device
CN103615717A (en) * 2013-10-24 2014-03-05 中国计量学院 Novel oxygen enrichment tiny-oil ignition and ultralow load stable-combustion combustor
US20170152830A1 (en) * 2014-07-21 2017-06-01 Apojee Ignition unit and system
CN208025504U (en) * 2018-01-26 2018-10-30 山东大学 A kind of coal burner

Patent Citations (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2002228107A (en) * 2001-01-31 2002-08-14 Mitsubishi Heavy Ind Ltd Pulverized coal burner
CN101021319A (en) * 2007-02-26 2007-08-22 杭州意能节能技术有限公司 Concentrated and thin fuel-saving igniting coal powder burner
CN101403497A (en) * 2008-11-12 2009-04-08 哈尔滨工业大学 Micro-oil ignition rotational flow breeze combustion device for preventing slag bonding of primary combustion chamber
CN201615480U (en) * 2010-02-09 2010-10-27 济南海普电力节能科技有限公司 Pulverized coal boiler microwave plasma preheating pulverized coal gasification small oil gun ignition device
CN103615717A (en) * 2013-10-24 2014-03-05 中国计量学院 Novel oxygen enrichment tiny-oil ignition and ultralow load stable-combustion combustor
US20170152830A1 (en) * 2014-07-21 2017-06-01 Apojee Ignition unit and system
CN208025504U (en) * 2018-01-26 2018-10-30 山东大学 A kind of coal burner

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN109140433A (en) * 2018-08-21 2019-01-04 煤科院节能技术有限公司 A kind of bipyramid preventing primary air piping overheating deforming is against coal powder injection powder burner
CN109140433B (en) * 2018-08-21 2024-04-19 北京天地融创科技股份有限公司 Double-cone reverse-injection pulverized coal burner capable of preventing primary air pipe from overheat deformation
CN115247785A (en) * 2020-11-12 2022-10-28 王永 A plasma cracking combustion device
CN113028390A (en) * 2021-04-19 2021-06-25 煤科院节能技术有限公司 Small-capacity biomass powder fuel boiler

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